JP2003279168A - Refrigerating system, device for instantaneously freezing humidity - Google Patents

Refrigerating system, device for instantaneously freezing humidity

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JP2003279168A
JP2003279168A JP2002119905A JP2002119905A JP2003279168A JP 2003279168 A JP2003279168 A JP 2003279168A JP 2002119905 A JP2002119905 A JP 2002119905A JP 2002119905 A JP2002119905 A JP 2002119905A JP 2003279168 A JP2003279168 A JP 2003279168A
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pressure refrigerant
temperature
humidity
refrigerant liquid
low
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Takao Hara
隆雄 原
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Central Engineering Kk
セントラル・エンジニアリング株式会社
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Abstract

PROBLEM TO BE SOLVED: To provide a refrigerating system, a device for instantaneously freezing humidity reducing equipment cost of an air cooling system and saving energy by reducing size and weight of an evaporator heat exchanging device to contribute protection of each environment.
SOLUTION: High temperature high pressure refrigerant gas discharged from a compressor 1 is sent to a condenser 3. When middle temperature high pressure refrigerant liquefied gas cooled by a fan 15 passes through spiral fine tube 9, the same is transformed to normal temperature middle pressure refrigerant liquid. After that, the normal temperature middle pressure refrigerant liquid pass through series of two spiral fine tubes 12 to be transformed to super low temperature low pressure refrigerant liquid and to be very quickly sent to a probe 11. Consequently, temperature and humidity can be instantaneously dropped when air 16 compressed by an air compressor is sent to the probe 11.
COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、空気冷却システムに用いられる湿度瞬時氷結装置に関する。 BACKGROUND OF THE INVENTION [0001] [Technical Field of the Invention The present invention relates to humidity instantaneous freezing apparatus for use in an air cooling system. 【0002】 【従来の技術】現在、一般に使用されている空気冷却システムは、図2に示される様に、冷房サイクル中に封入された冷媒フロンを圧縮機1で高温高圧の冷媒ガスにして、大きい放熱盤3(コンデンサー)で空気冷却させ凝縮液化(一部ガス状態のまま)させて、液タンク5・導管6を経てドライヤー7・導管8を経て膨張弁9で減圧膨張させ低圧の冷媒液ガスとし、この冷媒液ガスを蒸発器13に送り熱交換させる(庫内を冷却する)事により、蒸発気化し低圧冷媒ガスとなり圧縮機1に戻す用にした物である。 [0002] Currently, commonly used air cooling system, as shown in Figure 2, the refrigerant Freon encapsulated in a cooling cycle in the compressor 1 and the high-temperature high-pressure refrigerant gas, greater heat dissipation board 3 was air cooled condensed (part remains in a gaseous state) are allowed in (condenser) refrigerant liquid of the low pressure is decompressed and expanded by the expansion valve 9 through the dryer 7-conduit 8 through the liquid tank 5, a conduit 6 and gas, by which the refrigerant liquid gas evaporator 13 to thereby feed heat exchanger (a cooling in the refrigerator), and vaporized is obtained by the use of returning to the compressor 1 becomes a low-pressure refrigerant gas. 【0003】この様な従来の空気冷却システムにおいては、蒸発器13内で空気冷却を瞬時に出来ない為に大型構造とならざるを得ない事から、装置のコンパクト化を図る為に蒸発器13を小型化に色々と検討が成されているが、現状の空気冷却システムでは、熱交換面積を大幅に減らす事は技術的に困難であり依然として大型の蒸発器13が用いられている。 [0003] In such a conventional air cooling system, since it inevitably a large structure in order to not be the air cooling in an instant in the evaporator 13, the evaporator in order to reduce the size of the apparatus 13 the Although variously studied miniaturization have been made, in the current state of the air cooling system, to reduce the heat exchange area considerably is is used technically difficult still large evaporator 13. 【0004】 【発明が解決しようとする課題】本発明は、従来の空気冷却システムが抱える問題点の解消を図る為、蒸発器熱交換装置を小型・軽量化を図って空気冷却システムにおける装置、コスト低減化並びに省エネルギー化を推進させ、地球環境の保全に一翼を担わせる事が出来る冷凍冷却システム・湿度瞬時氷結装置を提供する事にある。 [0004] [SUMMARY OF THE INVENTION The present invention, conventional for achieving elimination of air cooling system faced problems, an apparatus in an air cooling system an evaporator heat exchanger and reduction in size and weight, cost reduction and to promote energy saving, is to provide a refrigeration cooling system and humidity instantaneous freezing apparatus able to play a role to protect the global environment. 【0005】本発明は、先に特開平10−259958 The present invention, Japanese Patent Laid-Open previously 10-259958
号明細書に置いて、キャピラリコイルの減圧膨張装置を高度の運動エネルギーに変換させる機能を有する熱変換装置を使用する事により、従来の蒸発器13と比較すると20分の1の面積になり、スペースも最小限ですみ電気使用量も2分の1ですむ。 No. placed herein, by using the heat converter having a function of converting the pressure reducing expansion device of the capillary coil to a high degree of kinetic energy results in one area of ​​20 minutes when compared to the conventional evaporator 13, electricity consumption is minimal even space also requires only 1 of 2 minutes. 【0006】 【課題を解決するための手段】本発明は、上記の目的を達成する為、以下に述べる構成とした物である。 [0006] The present invention SUMMARY OF], in order to achieve the above object is obtained by the configuration described below. 即ち本発明における請求項1の発明は、冷凍冷却システムに関する物で、圧縮機1から吐出した高温高圧冷媒ガスを凝縮器3に送りファン15で冷却した中温高圧冷媒液ガスが螺旋状細菅9内を通過すると常温中圧冷媒液に変化し後に、二連の螺旋状細菅12を通過すると超低温低圧冷媒液に変化し、非常に速くプローブ11に送り込まれ、 That invention of claim 1 of the present invention relates to a refrigeration cooling system, the compressor 1 to the condenser 3 the high-temperature high-pressure refrigerant gas discharged from the feed fan 15 medium-temperature high-pressure refrigerant liquid gas spiral Hososuga 9 cooled with passes through the inner later changed to room temperature during pressure refrigerant liquid, passes through the helical Hososuga 12 duplicate changed to ultra low temperature and low pressure refrigerant liquid is fed into the very fast probe 11,
エアーコンプレッサーで加圧した空気16をプローブ1 Probe pressurized air 16 in the air compressor 1
1内に送り込まれた時に、瞬時に温度・湿度を低温にさせる事が出来る冷凍冷却システム・瞬時湿度氷結装置を使用している事を特徴とする。 When fed into the 1, characterized in that using refrigeration cooling system instantaneous humidity icing device it is possible to the temperature and humidity in the low-temperature instantaneously. 【0007】また、本発明における請求項2の発明は、 [0007] The invention of claim 2 of the present invention,
運動エネルギーを使用し凝縮器3から出た中温高圧冷媒液ガスを螺旋状細菅9にて加速・スピン回転・引圧機能を持つミニ装置を経て完全液化し、減圧膨張弁より性能の良い二連の螺旋状細菅12を使い低温低圧冷媒液を作り冷媒量を多く押し出し瞬時に空気・湿度を低温にする、冷凍冷却システム・湿度瞬時氷結装置を特徴とする。 The use of kinetic energy exiting from the condenser 3 medium-temperature high-pressure refrigerant liquid gas via a mini device having an acceleration-spin rotation and suction pressure function in spiral Hososuga 9 completely liquefied, good performance from the pressure reducing expansion valve two the air-humidity to low temperatures immediately extruded increase the refrigerant quantity making the low-temperature and low-pressure refrigerant liquid using a spiral Hososuga 12 of the communication, and wherein the refrigeration cooling system humidity instantaneous freezing apparatus. 【0008】この様な本発明によれば、冷凍冷却システムにおける凝縮行程での熱変換機能と蒸発行程での加速・引圧機能を兼ね備えている物と、使用されている現行の空気冷却システムのそれとは全く異なっている点に特徴があり、基本的には高温高圧冷媒ガスに対して高速・ [0008] According to such a present invention, and those which have both an acceleration and suction pressure function in the heat conversion function and the evaporation process in the condensation process in the refrigeration cooling system, the current being used for the air cooling system it and is characterized in that is quite different from, basically speed and relative high-temperature high-pressure refrigerant gas
スピン回転・引圧作用を成す過程において熱放熱が他のエネルギーで出来る事に着目し、それを冷凍冷却システムの凝縮行程・蒸発行程に応用する事によって、凝縮・ By heat radiator is focused on it that can be in other energy in the process of forming the spinning-suction pressure acting to apply it to the condensation process and evaporation stroke of the refrigeration cooling system, condensed and
液化・減圧の為に必要な熱源の大部分を循環冷媒自体に求める用にした点に本発明の特徴とする。 And features of the present invention the majority of the heat source necessary for liquefaction and decompression in that the use for determining the circulating refrigerant itself. 【0009】即ち、本発明に係る新規な冷凍冷却システムでは、液化させる為の運動エネルギー方式を使用し、 [0009] That is, a novel refrigeration cooling system according to the present invention uses the kinetic energy method for liquefying,
減圧膨張弁の替わりに高速・スピン回転・引圧作用を用いる事により液変換が出来、最大級に冷凍能力を持つ冷媒液にする方式を採用した点を特徴としている。 Liquid conversion can by using a fast-spinning, a suction pressure acts in place of the pressure reducing expansion valve, and is characterized in that employing the method of the refrigerant liquid having a refrigeration capacity to the largest. この事は、研究及び実験を重ねた結果に基づいて充分に確認された所であり、また、発明の実施形態の説明によっても明らかにされる。 This is where confirmed sufficiently on the basis of a result of extensive studies and experiments, also be revealed by the description of embodiments of the invention. 【0010】 【発明の実施の形態】以下、本発明の実施形態の好ましい例について添付図面を参照しながら説明する。 DETAILED DESCRIPTION OF THE INVENTION Hereinafter, will be described with reference to the accompanying drawings a preferred example of an embodiment of the present invention. 図1には、本発明の実施形態に係る冷凍冷却システムの冷凍回路が示される。 1 shows a refrigeration circuit of a refrigeration cooling system according to an embodiment of the present invention is shown. 冷凍冷却システムは、圧縮機1と凝縮器3と完全液化装置・螺旋状細菅9と減圧膨張弁の替わりに二連の螺旋状細菅12とプローブ11とを要素機器として備え、それら機器を冷媒配管によって循環的に接続する事によって冷凍冷却システムの装置が構成される。 Refrigeration cooling system comprises a compressor 1 and the condenser 3 and the full liquefier-helical Hososuga 9 spiral Hososuga 12 instead of duplicate of the pressure reducing expansion valve and probe 11 as an element device, their equipment the apparatus of refrigeration cooling system by circulating connected by refrigerant pipes constructed. 【0011】圧縮機1、及び凝縮器3は、現行の空気冷却システムに使用される物と構造、機能が基本的に変わらないので、ここでは詳細な説明を省略し、本発明の特徴とされる構成要素である完全液化装置・螺旋状細管9 [0011] compressor 1, and the condenser 3, since things and structures used in the current air cooling system, function essentially unchanged, where a detailed description is omitted, is a feature of the present invention complete liquefier-spiral narrow tube 9 which is a component that
と運動エネルギーを使用する二連の螺旋状細菅12の態様について以下説明する。 It will be described below duplicate aspects of helical Hososuga 12 to use the kinetic energy. 【0012】上記、完全液化装置・螺旋状細菅9は例として数メートルの熱伝導性能に優れている細管、例として外径5ミリの銅管を螺旋状に巻き形成されていて、本実施形態の例では、螺旋状細菅9の内部を流れる冷媒液ガスを高速・スピン回転・僅かな減圧を行わせる事が出来、冷媒ガスを液化させる事が可能なミニ装置を特徴とされる。 [0012] The full liquefier-helical Hososuga 9 be formed wound copper tube having an outer diameter of 5 millimeters helically excellent and tubules example heat conduction performance of several meters as an example, the present embodiment in the example of embodiment, the refrigerant liquid gas flowing in the spiral Hososuga 9 able to perform a fast spin rotation and slight vacuum, is characterized in mini device capable of liquefying the refrigerant gas. 【0013】上記、二連の螺旋状細菅12、例として数メートルの熱伝導性能に優れている細菅例として外径3 [0013] The outer diameter as Hososuga example has excellent thermal conductivity performance of several meters as helical Hososuga 12, examples of duplicate 3
ミリの銅管を螺旋状に巻き形成されていて、本実施形態の例では、螺旋状細菅の内部を流れる冷媒液を高速・スピン回転・引圧作用を用いる事により、冷媒液が瞬時に超低温・低圧冷媒液に変化する事を特徴とされる。 The copper tube of a millimeter have been wound spirally formed, in the example of this embodiment, a refrigerant liquid flowing in the spiral Hososuga by using a fast-spinning, the suction pressure acts, the refrigerant liquid is instantaneously It is characterized in that changes to the ultra low-temperature low-pressure refrigerant liquid. 【0014】なお、本発明において重要な構成要素部材である螺旋状細菅9と二連の螺旋状細菅12は、用いられる金属の材質、菅の長さ及び径、螺旋の径、ピッチ及び巻き方向の各条件について、数々の試験を重ねる事により細管を設定すれば良いこの場合、所定サイズの細菅の1本を螺旋状に加工した物、巻き方向が異なる螺旋状細菅の2本の直列・並列に接続した物等のいずれにしても細菅の螺旋状が必要であり、高速・スピン回転・引圧・熱変換を効率的に成し得る条件の螺旋状細菅を随時選択すれば良い。 [0014] Incidentally, the helical Hososuga 9 spiral Hososuga 12 duplicate a key component member in the present invention, the material of the metal used, the length and diameter of the Kan, the diameter of the spiral, the pitch and for each condition in the winding direction, if this is sufficient to set the tubules by overlaying a number of tests, those obtained by processing helically one Hososuga of a predetermined size, two of the winding direction different spiral Hososuga of Whichever object or the like connected in series-parallel are required Hososuga spiral, from time to time select the spiral Hososuga conditions can make high-speed spinning, the suction pressure-heat conversion efficient it is sufficient. 【0015】 【実施例】上記、第一実施例においてフロン冷媒R−2 [0015] [Example] above, Freon refrigerant R-2 in the first embodiment
2を用いた具体的な実施装置に関して、その各部における冷媒の圧力・温度の状態は図1を参照して、中温・高圧冷媒ガス(イ)1.1パスカル35度・高圧冷媒液ガス(ロ)1.1パスカル33度・高圧冷媒液ガス(ハ) With regard to specific embodiments devices using 2, pressure and temperature state of the refrigerant in the respective units with reference to FIG. 1, the medium-temperature, high-pressure refrigerant gas (a) 1.1 Pascal 35 °-pressure refrigerant liquid gas (B ) 1.1 Pascal 33 degrees-pressure refrigerant liquid gas (c)
1.1パスカル31度・高圧冷媒液ガス(ニ)1.1パスカル31度・高圧冷媒液ガス(ホ)1.1パスカル3 1.1 Pascal 31 °-pressure refrigerant liquid gas (d) 1.1 Pascal 31 °-pressure refrigerant liquid gas (e) 1.1 Pascal 3
0度・中圧冷媒液(ヘ)0.7パスカル18度・低温低圧冷媒液(ト)0.25パスカル−10度・低温低圧冷媒ガス(チ)0.25パスカル0度・となる。 0 degree - medium-pressure liquid refrigerant becomes (f) 0.7 Pascal 18 degrees, the low-temperature low-pressure refrigerant liquid (g) 0.25 Pascal -10 °-temperature low-pressure refrigerant gas (h) 0.25 Pascal 0 ° -. 【0016】なお上記、第二実施例においてフロン冷媒R−22を用いた具体的な実施装置に関して、その各部における冷媒の圧力・温度の状態は図2を参照して、高温・高圧冷媒ガス(イ)1.8パスカル85度・高温・ [0016] Note that the above, with regard to specific embodiments devices using Freon refrigerant R-22 in the second embodiment, the pressure and temperature state of the refrigerant in the respective units with reference to FIG. 2, high-temperature high-pressure refrigerant gas ( b) 1.8 Pascal 85 degrees, high temperature,
高圧冷媒液ガス(ロ)1.8パスカル50度・高圧冷媒液ガス(ハ)1.8パスカル47度・高圧冷媒液ガス(ニ)1.8パスカル47度・高圧冷媒液ガス(ホ) High-pressure refrigerant liquid gas (b) 1.8 Pascal 50 °-pressure refrigerant liquid gas (c) 1.8 Pascal 47 °-pressure refrigerant liquid gas (d) 1.8 Pascal 47 °-pressure refrigerant liquid gas (e)
1.8パスカル45度・低圧冷媒液ガス(ヘ)0.5パスカル12度・低圧冷媒液ガス(ト)0.5パスカル2 1.8 Pascal 45 °-pressure refrigerant liquid gas (f) 0.5 Pascal 12 degrees-pressure refrigerant liquid gas (g) 0.5 Pascal 2
0度・中温低圧冷媒ガス(チ)0.5パスカル25度・ 0 degree - medium-temperature low-pressure refrigerant gas (h) 0.5 Pascal 25 degrees,
となる。 To become. 【0017】(発明の効果)本発明は、以上説明した様な形態で実施させ、以下に記載される様な効果を奏する。 [0017] (Effect of the Invention) The present invention is carried out in the described such form above, it exhibits the kind of effect as described below. 即ち、本発明によれば、蒸発器13で瞬時空気冷却が出来ない為に大型構造とならざるを得ない原因であった点に着目し、新規な冷凍冷却システム・湿度瞬時氷結装置の完成に基づき蒸発用熱交換面積の飛躍的な縮小を図る事を可能とし、空気・湿度を瞬時に過冷却出来る為に、ネジ切・フライス加工・NC旋盤などのオイル冷却を取り除き産業廃棄物を無くし、空気・湿度冷却で通常のオイル冷却より2倍以上の加工が出来産業界に寄与する所、正に多大な発明である。 That is, according to the present invention, paying attention to the point were responsible for inevitably a large structure for not be instantaneous air cooled by the evaporator 13, to the completion of the new refrigeration cooling system and humidity instantaneous icing device based to enable it to achieve dramatic reduction in evaporative heat exchange area, in order to be supercooled air and humidity instantly eliminate industrial waste removed oil cooling, such as screws switching-milling, NC lathe, contributing plants in the industry can conventional oil cooling from the machining of more than double in the air and humidity cooling is just great invention.

【図面の簡単な説明】 【図1】本発明の実施の形態に係る冷凍冷却システム・ Refrigeration cooling system according to the embodiment of the drawings: Figure 1 of the present invention,
湿度瞬時氷結装置の回路図である。 It is a circuit diagram of the humidity instantaneous freezing apparatus. 【図2】従来の空気冷却システムの構成図である。 2 is a block diagram of a conventional air cooling system. 【符号の説明】 1=圧縮機 2=導管 3=凝縮器4=導管 5=レシーバータンク 6=導管7=ドライヤー 8=導管 9=螺旋状細菅10=導管 11=プローブ 12=二連の螺旋状細菅13=蒸発器 14=サクション菅 15=ファン16=空気 [EXPLANATION OF SYMBOLS] 1 = compressor 2 = line 3 = condenser 4 = conduit 5 = receiver tank 6 = conduit 7 = dryers 8 = conduit 9 = helical Hososuga 10 = line 11 = probe 12 = duplicate helix JoHososuga 13 = evaporator 14 = suction Kan 15 = fan 16 = air

Claims (1)

  1. 【特許請求の範囲】 【請求項1】 圧縮機1から吐出した高温高圧冷媒ガスが導管2を経て、通常の凝縮器3に送り空気冷却をした中温(常温より高い温度)高圧冷媒ガスが導管4を経て、レシーバータンク5に送り導管6を経てドライヤー7(水分・カスなど取去る)に送り、導管8を経て中温高圧冷媒液・ガスは螺旋状細菅9内を通過し導管10に至る時は常温中圧冷媒液に変化した後に二連の螺旋状細菅12を経て超低温低圧冷媒液が非常に速くプローブ1 Through Patent Claims 1. A high-temperature high-pressure refrigerant gas discharged from the compressor 1 is a conduit 2, the normal condenser 3 to the feed medium temperature in which the air cooling (temperature higher than the room temperature) the high pressure refrigerant gas conduit 4 through, via a conduit 6 feeding the receiver tank 5 is sent to the dryer 7 (etch away moisture Kass), medium-temperature high-pressure refrigerant liquid gas via conduit 8 leads to the conduit 10 through the spiral Hososuga 9 when the dual helical Hososuga 12 through the ultra-low temperature and low pressure refrigerant liquid probe very quickly after the change in the ambient temperature during pressure refrigerant liquid 1
    1の内側に螺旋回転している銅管内に低温低圧冷媒液を通過させプローブ11内にエアーコンプレッサーで加圧した空気16を送りプローブ11内を通過した時に瞬時に湿度を低温にし放出させる事が出来る様にし、サクション菅14に導き圧縮機1に吸入させる冷凍冷却システム・湿度瞬時氷結装置。 Instantaneously to emit humidity cold when passed through the pressurized feed air 16 within the probe 11 with the air compressor in the probe 11 is passed through a low-temperature low-pressure refrigerant liquid to the copper tube are helical rotation inside the 1 and in the manner possible, refrigeration cooling system and humidity instant freezing equipment and to be taken in by the compressor 1 led to the suction tube 14. 【請求項2】 凝縮器から出た中温高圧冷媒ガスを螺旋状細菅9にて加速・スピン回転・引圧機能を持つミニ装置を経て、完全液化し次に、減圧膨張弁の替わりに二連の螺旋状細菅12を使用し運動エネルギーを使い低音低圧冷媒液を作り量多く押し出し瞬時に空気・湿度を低温にする冷凍冷却システム・湿度瞬時氷結装置。 2. Through the mini device having an acceleration-spin rotation and suction pressure function mesophilic high-pressure refrigerant gas discharged from the condenser in a spiral Hososuga 9, fully liquefied in the following, instead of the pressure reducing expansion valve two communicating helical Hososuga 12 refrigeration cooling system and humidity instantaneous freezing apparatus the air humidity amounts to make a bass low pressure refrigerant liquid to use the kinetic energy much in extrusion instantly used to low temperature.
JP2002119905A 2002-03-19 2002-03-19 Refrigerating system, device for instantaneously freezing humidity Pending JP2003279168A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1930669A1 (en) * 2005-09-26 2008-06-11 Hara Tech Corporation Thermal converter for condensation and refrigeration system using the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1930669A1 (en) * 2005-09-26 2008-06-11 Hara Tech Corporation Thermal converter for condensation and refrigeration system using the same
US20090241591A1 (en) * 2005-09-26 2009-10-01 Takao Hara Heat converter for condensation and refrigeration system using the same
EP1930669A4 (en) * 2005-09-26 2013-09-18 Hara Tech Corp Thermal converter for condensation and refrigeration system using the same
KR101319198B1 (en) * 2005-09-26 2013-10-16 다까오 하라 Thermal converter for condensation and refrigeration system using the same
US8746007B2 (en) * 2005-09-26 2014-06-10 Takao Hara Heat converter for condensation and refrigeration system using the same

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